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  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L23/10—Homopolymers or copolymers of propene
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  • C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
  • C08J5/18—Manufacture of films or sheets
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B27/00—Layered products comprising a layer of synthetic resin
  • B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
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  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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  • C08F4/00—Polymerisation catalysts
  • C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
  • C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
  • C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
  • C08F4/62—Refractory metals or compounds thereof
  • C08F4/64—Titanium, zirconium, hafnium or compounds thereof
  • C08F4/642—Component covered by group C08F4/64 with an organo-aluminium compound
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  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L23/04—Homopolymers or copolymers of ethene
  • C08L23/06—Polyethene
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  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L23/10—Homopolymers or copolymers of propene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L23/10—Homopolymers or copolymers of propene
  • C08L23/14—Copolymers of propene
  • C08L23/142—Copolymers of propene at least partially crystalline copolymers of propene with other olefins
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  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
  • C09J123/00—Adhesives based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Adhesives based on derivatives of such polymers
  • C09J123/02—Adhesives based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Adhesives based on derivatives of such polymers not modified by chemical after-treatment
  • C09J123/10—Homopolymers or copolymers of propene
  • C09J123/14—Copolymers of propene
  • C09J123/142—Copolymers of propene at least partially crystalline copolymers of propene with other olefins
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
  • C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
  • C08J2323/04—Homopolymers or copolymers of ethene
  • C08J2323/08—Copolymers of ethene
• • C—CHEMISTRY; METALLURGY
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  • C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
  • C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
  • C08J2323/10—Homopolymers or copolymers of propene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L2314/00—Polymer mixtures characterised by way of preparation
  • C08L2314/06—Metallocene or single site catalysts
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L2666/00—Composition of polymers characterized by a further compound in the blend, being organic macromolecular compounds, natural resins, waxes or and bituminous materials, non-macromolecular organic substances, inorganic substances or characterized by their function in the composition
  • C08L2666/02—Organic macromolecular compounds, natural resins, waxes or and bituminous materials
  • C08L2666/04—Macromolecular compounds according to groups C08L7/00 - C08L49/00, or C08L55/00 - C08L57/00; Derivatives thereof
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  • Y10S428/00—Stock material or miscellaneous articles
  • Y10S428/91—Product with molecular orientation
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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  • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10S526/00—Synthetic resins or natural rubbers -- part of the class 520 series
  • Y10S526/943—Polymerization with metallocene catalysts
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
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  • Y10T428/00—Stock material or miscellaneous articles
  • Y10T428/24—Structurally defined web or sheet [e.g., overall dimension, etc.]
  • Y10T428/24942—Structurally defined web or sheet [e.g., overall dimension, etc.] including components having same physical characteristic in differing degree
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  • Y10T428/24967—Absolute thicknesses specified
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  • Y10T428/26—Web or sheet containing structurally defined element or component, the element or component having a specified physical dimension
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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  • Y10T428/28—Web or sheet containing structurally defined element or component and having an adhesive outermost layer
  • Y10T428/2852—Adhesive compositions
  • Y10T428/2878—Adhesive compositions including addition polymer from unsaturated monomer
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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  • Y10T428/31504—Composite [nonstructural laminate]
  • Y10T428/31725—Of polyamide
  • Y10T428/31739—Nylon type
  • Y10T428/31743—Next to addition polymer from unsaturated monomer[s]
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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  • Y10T428/31786—Of polyester [e.g., alkyd, etc.]
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  • Y10T428/31913—Monoolefin polymer
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Definitions

• the present invention relates to a laminating propylene/1-butene random copolymer composition which is suitable for use in a laminate layer of a composite film and relates to a composite film formed using the composition.
• the crystalline polypropylene film is excellent in mechanical properties such as tensile strength, rigidity, surface hardness, impact resisting strength and cold resistance, optical properties such as gloss and transparency and food sanitation properties such as nontoxicity and odorlessness.
• the crystalline polypropylene film is widely employed in the field of, especially, food.
• the crystalline polypropylene film is high in the heat sealing temperature and small in the range thereof, so that there occur problems of poor welding of heat seal portions and fusion thereof.
• a propylene/1-butene random copolymer is used as the resin capable of forming the resin layer which is to become a heat seal portion. It is known that this copolymer has excellent transparency and low-temperature sealing properties and has relatively good blocking resistance.
• the present invention has been made with a view toward solving the above problems of the prior art, and the object of the present invention is to provide a propylene/1-butene random copolymer composition suitable for a laminate molding of a composite film which is excellent in low-temperature sealing properties and blocking resistance and to provide the composite film thereof.
• the laminating propylene/1-butene random copolymer composition of the present invention comprises 50 to 97% by weight of a propylene/1-butene random copolymer (A) and 50 to 3% by weight of a low-density polyethylene (B), the above propylene/1-butene random copolymer (A):
• the propylene/1-butene random copolymer (A) may be obtained by copolymerizing propylene and 1-butene in the presence of an olefin polymerization catalyst, the above olefin polymerization catalyst comprising:
• the composite film of the present invention comprises a substrate film and, laminated onto at least one side thereof, a resin layer of the above laminating propylene/1-butene random copolymer composition of the present invention, the above resin layer having a thickness of 2 to 200 ⁇ m.
• the laminating propylene/1-butene random copolymer composition of the present invention comprises a propylene/1-butene random copolymer (A) and a low-density polyethylene (B).
• the propylene/1-butene random copolymer (A) for use in the present invention comprises:
• the propylene/1-butene random copolymer (A) may contain structural units derived from an olefin other than propylene and 1-butene in a small amount of, for example, not greater than 10 mol%, preferably, not greater than 5 mol%.
• the propylene/1-butene random copolymer (A) for use in the present invention exhibits a melt flow rate (measured at 230°C under a load of 2.16 kg in accordance with ASTM D 1238) of 0.1 to 40 g/10 min, preferably, 0.5 to 30 g/10 min and, still preferably, 1 to 20 g/10 min.
• the propylene/1-butene random copolymer (A) for use in the present invention has a molecular weight distribution (Mw/Mn), measured by gel permeation chromatography (GPC), of up to 3, preferably, up to 2.5.
• Mw/Mn molecular weight distribution measured by gel permeation chromatography
• the propylene/1-butene random copolymer (A) for use in the present invention has a B-value, being a parameter indicating a randomness of copolymer monomer chain distribution, of 1.0 to 1.5, preferably, 1.0 to 1.3 and, still preferably, 1.0 to 1.2.
• B P 12 /(2P 1 -P 2 ) wherein P 1 and P 2 represent first monomer and second monomer content fractions, respectively, and P 12 represents the proportion of (first monomer)-(second monomer) chains to all bimolecular chains.
• the B-value is 1, the Bernoulli's statistics applies.
• the B-value is smaller than 1 (B ⁇ 1), the copolymer is arranged in the form of block chains.
• the B-value is greater than 1 (B > 1), the copolymer is arranged in the form of alternate chains.
• the propylene/1-butene random copolymer (A) for use in the present invention have a melting point (Tm), measured by a differential scanning calorimeter, of 60 to 140°C, especially, 80 to 130°C. It is also preferred that the above melting point, Tm, and a content of 1-butene structural units, M (mol%), satisfy the relationship: -2.6 M + 130 ⁇ Tm ⁇ -2.3 M + 155.
• the suitable film heat sealing temperature becomes as high as 130°C or above.
• the melting temperature is lower than 60°C, the scratch resistance is deteriorated although the low-temperature heat sealing properties are improved and, further, film blocking may occur during the storage, thereby rendering the practical use difficult.
• the propylene/1-butene random copolymer (A) preferably has a crystallinity measured by X-ray diffractometry, C(%), this crystallinity and the content of 1-butene structural units, M (mol%), satisfying the relationship: C ⁇ -1.5 M + 75.
• the crystallinity of the propylene/1-butene random copolymer (A) preferably ranges from 15 to 65%, still preferably, from 20 to 60%.
• the propylene/1-butene random copolymer (A) for use in the present invention may contain position irregular units attributed to 2,1-insertion of propylene monomer in a ratio to all propylene structural units of 0.05% or more, which ratio can be determined by 13 C-NMR spectrum.
• the propylene monomer In the polymerization, the propylene monomer rarely undergoes 2,1-insertion although it generally undergoes 1,2-insertion (methylene side is bonded with the catalyst).
• the 2,1-inserted monomer forms position irregular units in the polymer.
• peaks were designated according to the method of Carman et al. (Rubber Chem. Technol., 44 (1971), 781). I ⁇ and the like represent the area of peak ⁇ and the like.
• the propylene/1-butene random copolymer (A) for use in the present invention may contain position irregular units attributed to 1,3-insertion of propylene monomer in an amount of up to 0.05%.
• the amount of 3 consecutive chains attributed to 1,3-insertion of propylene can be determined by ⁇ peak (resonance at about 27.4 ppm).
• the above propylene/1-butene random copolymer (A) can be obtained by copolymerizing propylene and 1-butene in the presence of an olefin polymerization catalyst (metallocene catalyst) comprising:
• Transition metal compound metalocene compound
• the above transition metal compound (a) is represented by the general formula:
• M represents a transition metal of Group IVa, Va or VIa of the periodic table.
• Preferred examples thereof include titanium, zirconium and hafnium. Of these, zirconium is especially preferred.
• Each of R 1 and R 2 independently represents a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, a halogenated hydrocarbon group having 1 to 20 carbon atoms, a silicon-containing group, an oxygen-containing group, a sulfur-containing group, a nitrogen-containing group or a phosphorus-containing group.
• Each of R 3 independently represents a hydrocarbon group having 1 to 20 carbon atoms, which may be substituted with a halogen atom or a silicon-containing group.
• R 3 represent a secondary or tertiary alkyl group having 3 to 20 carbon atoms or an aromatic group having 6 to 20 carbon atoms.
• Each of R 4 independently represents a hydrogen atom or an alkyl group having 1 to 20 carbon atoms. This alkyl group may be substituted with a halogen atom or a silicon-containing group.
• Each of X 1 and X 2 independently represents a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, a halogenated hydrocarbon group having 1 to 20 carbon atoms, an oxygen-containing group or a sulfur-containing group.
• Y represents a divalent hydrocarbon group having 1 to 20 carbon atoms, a divalent halogenated hydrocarbon group having 1 to 20 carbon atoms, a divalent silicon-containing group, a divalent germanium-containing group, a divalent tin-containing group, -O-, -CO-, -S-, -SO-, -SO 2 -, etc.
• Y represent an alkylsilylene, an alkylarylsilylene or an arylsilylene.
• transition metal compounds (a) of the general formula [I] those wherein R 1 is a methyl group are especially preferred.
• a multiplicity of specific examples of the transition metal compounds (a) represented by the general formula (I) are set forth in Japanese Patent Laid-open Publication No. 8(1996)-238729.
• Aluminooxanes are preferably used as the above organoaluminum oxy compound (b-1).
• b-1 organoaluminum oxy compound
• methylaluminooxane, ethylaluminooxane, methylethylaluminooxane and the like which individually have generally about 3 to 50 repeating units represented by the formula: -Al(R)O- wherein R represents an alkyl group.
• R represents an alkyl group.
• organoaluminum oxy compound (b-1) may be benzene-insoluble organoaluminum oxy compounds listed by way of example in Japanese Patent Laid-open Publication No. 2(1990)-78687.
• Examples of the compounds (ionizing ionic compounds) (b-2) capable of reacting with the transition metal compound (a) to thereby form an ion pair, employed in the present invention, include Lewis acids listed in U.S. Patent No. 5,321,106 such as triphenylboron, MgCl 2 , Al 2 O 3 and SiO 2 -Al 2 O 3 .
• ionizing ionic compounds (b-2) can be used either individually or in combination.
• organoaluminum compounds (c) employed according to necessity in the present invention include trialkylaluminums, dialkylaluminum halides, alkylaluminum sesqihalides and alkylaluminum dihalides.
• organoaluminum compounds can be used either individually or in combination.
• the olefin polymerization catalyst for use in the present invention is formed from the above transition metal compound (a), organoaluminum oxy compound (b-1) and/or ionizing ionic compound (b-2), and optionally the organoaluminum compound (c).
• the olefin polymerization catalyst can be prepared by mixing in an inert hydrocarbon solvent or an olefin solvent the above transition metal compound (a), organoaluminum oxy compound (b-1) and/or ionizing ionic compound (b-2), and optionally the component (c).
• an olefin prepolymerization can be conducted in the above olefin polymerization catalyst forming components before the use thereof.
• Suitable olefins used in the prepolymerization include propylene, ethylene and 1-butene. However, also, use can be made of mixtures thereof with other olefins.
• the propylene/1-butene random copolymer (A) for use in the present invention can be produced by copolymerizing propylene and 1-butene in the presence of the above olefin polymerization catalyst.
• This polymerization can be performed by any of the liquid phase polymerization techniques such as suspension polymerization technique and solution polymerization technique and the vapor phase polymerization technique.
• the molecular weight of the obtained propylene/1-butene random copolymer (A) can be regulated by causing hydrogen to be present in the polymerization system or by changing the polymerization temperature and polymerization pressure.
• the propylene/1-butene random copolymer (A) is used in an amount of 50 to 97% by weight, preferably, 55 to 96% by weight and, still preferably, 60 to 95% by weight based on 100 % by weight of the sum of the propylene/1-butene random copolymer (A) and the low-density polyethylene (B).
• the low-density polyethylene (B) for use in the present invention is preferably an ethylene homopolymer or a copolymer of ethylene and an ⁇ -olefin having 3 to 20 carbon atoms, and the density thereof is preferably not greater than 0.940 g/cm 3 , still preferably, in the range of 0.915 to 0.935 g/cm 3 and, yet still preferably, in the range of 0.916 to 0.925 g/cm 3 .
• ⁇ -olefin is, for example, selected from among propylene, 1-butene, 1-pentene, 2-methyl-1-butene, 3-methyl-1-butene, 1-hexene, 3-methyl-1-pentene, 4-methyl-1-pentene, 3,3-dimethyl-1-butene, 1-heptene, methyl-1-hexene, dimethyl-1-pentene, trimethyl-1-butene, ethyl-1-pentene, 1-octene, methyl-1-pentene, dimethyl-1-hexene, trimethyl-1-pentene, ethyl-1-hexene, methylethyl-1-pentene, diethyl-1-butene, propyl-1-pentene, 1-decene, methyl-1-nonene, dimethyl-1-octene, trimethyl-1-heptene, ethyl-1-octene, methylethyl-1-heptene,
• ⁇ -olefins can be used either individually or in combination.
• the low-density polyethylene (B) for use in the present invention exhibits a melt flow rate (MFR; measured at 190°C under a load of 2.16 kg in accordance with ASTM D 1238) of 1 to 30 g/10 min, preferably, 1 to 25 g/10 min and, still preferably, 3 to 20 g/10 min.
• MFR melt flow rate
• the above low-density polyethylene (B) can be produced by conventional processes, for example, the high pressure process.
• the production of the low-density polyethylene (B) with the above properties can be conducted in the presence of metallocene catalyst.
• the low-density polyethylene (B) is used in an amount of 50 to 3% by weight, preferably, 45 to 4% by weight and, still preferably, 40 to 5% by weight based on 100 % by weight of the sum of the propylene/1-butene random copolymer (A) and the low-density polyethylene (B).
• the propylene/1-butene random copolymer (A) composition containing the low-density polyethylene (B) in the above amount exhibits excellent moldability without suffering from surging or neck-in enlargement even if the laminating speed is increased.
• the laminating propylene/1-butene random copolymer composition of the present invention can contain, in addition to the above propylene/1-butene random copolymer (A) and low-density polyethylene (B), various additives such as an antioxidant, an ultraviolet absorber, a lubricant, a nucleating agent, an antistatic agent, a flame retarder, a pigment, a dye and an organic or inorganic filler in an amount not detrimental to the object of the present invention.
• various additives such as an antioxidant, an ultraviolet absorber, a lubricant, a nucleating agent, an antistatic agent, a flame retarder, a pigment, a dye and an organic or inorganic filler in an amount not detrimental to the object of the present invention.
• the laminating propylene/1-butene random copolymer composition of the present invention can be prepared by any of common blending techniques.
• the composition can be prepared by mixing the above components by means of a mixing machine such as a V-blender, a ribbon blender or a Henschel mixer, or by kneading the above components by a kneading machine such as an extruder, a mixing roll mill, a Banbury mixer or a kneader.
• a mixing machine such as a V-blender, a ribbon blender or a Henschel mixer
• kneading machine such as an extruder, a mixing roll mill, a Banbury mixer or a kneader.
• the laminating propylene/1-butene random copolymer composition of the present invention can also be prepared by mixing or kneading the above components by the use of the above mixing and kneading means in combination.
• the composite film of the present invention comprises a substrate film and, laminated onto at least one side thereof, a resin layer of the above laminating propylene/1-butene random copolymer composition of the present invention, the above resin layer having a thickness of 2 to 200 ⁇ m, preferably, 10 to 60 ⁇ m.
• polymers suitably used in the substrate film include:
• the polypropylene used in the molding of this polypropylene film be propylene homopolymer or a random or block copolymer of propylene and another ⁇ -olefin such as ethylene or 1-butene (generally, the content of propylene structural units is at least 90 mol%) whose boiling n-heptane insoluble content is at least 90%, especially, at least 93%.
• the above polypropylene can be produced with the use of, as a typical example, a catalyst composed of a solid titanium catalyst component and an organometallic compound catalyst component or a catalyst composed of these components and an electron donor.
• solid titanium catalyst component there can be mentioned, for example, a titanium trichloride or titanium trichloride composition produced by various methods, or a supported titanium catalyst component comprising magnesium, a halogen, an electron donor (preferably, an aromatic carboxylic acid ester or alkylated ether) and titanium as essential ingredients.
• a supported titanium catalyst component having a specific surface area of at least 100 m 2 /g is especially preferred.
• the above organometallic compound catalyst component is preferably an organoaluminum compound such as a trialkylaluminum, a dialkylaluminum halide, an alkylaluminum sesquihalide or an alkylaluminum dihalide.
• organoaluminum compound such as a trialkylaluminum, a dialkylaluminum halide, an alkylaluminum sesquihalide or an alkylaluminum dihalide.
• the suitability of such a compound as the catalyst component depends on the type of the titanium catalyst component.
• the organoaluminum compound for use be selected in conformity with the type of employed titanium catalyst component.
• the above electron donor is, for example, selected from among organic compounds containing nitrogen, phosphorus, sulfur, oxygen, silicon, boron, etc. Preferred examples thereof are esters and ethers.
• the crystalline polypropylene can be produced by the conventional process using the above conventional solid titanium catalyst component or metallocene compound catalyst component.
• polypropylene resin (A) either may a single variety be used individually or a plurality of different varieties may be used in combination.
• the composite film of the present invention can be produced, for example, by performing an extrusion coating of the above laminating propylene/1-butene random copolymer composition of the present invention through a T-die onto a substrate.
• the laminating propylene/1-butene random copolymer composition of the present invention is excellent in laminate moldability and enables producing a composite film having excellent low-temperature sealing properties, blocking resistance and hot tack.
• the composite film of the present invention has excellent low-temperature sealing properties, blocking resistance, slip properties and hot tack.
• separating column TSK GNH HT having a size of 27 mm in diameter and 600 mm in length.
• the column was heated at 140°C, and o-dichlorobenzene (produced by Wako Pure Chemical Industries Ltd.) and 0.025% by weight BHT (produced by Takeda Chemical Industries, Ltd.) were used as a mobile phase and an antioxidant, respectively.
• the moving velocity was set at 1.0 ml/min, and the sample concentration and injected sample quantity were 0.1% by weight and 500 ⁇ l, respectively.
• a differential refractometer was used as the detector.
• Standard polystyrene produced by Tosoh Corporation was used for molecular weights Mw ⁇ 1000 and Mw > 4 x 10 6
• standard polystyrene produced by Pressure Chemical was used for molecular weights Mw satisfying the relationship 1000 ⁇ Mw ⁇ 4 x 10 6 .
• DSC differential scanning calorimeter
• a 1.0 mm thick pressed sheet having been allowed to stand still for at least 24 hr after molding was analyzed by X-ray diffractometry from which the crystallinity was determined.
• the composite films obtained in the Examples and Comparative Examples were tested with respect to the haze, change of haze with the passage of time, gloss, slip properties, change of slip properties with the passage of time, blocking resistance, change of blocking resistance with the passage of time, interlayer bonding strength, heat sealing properties and hot tack. The following testing methods were employed.
• the composite film was held at 80°C for 3 days and allowed to cool, and its haze was measured in the same manner as in item (1) above.
• the composite film was annealed at 40°C for one day, and the coefficient of static friction and coefficient of dynamic friction of the surface of the layer of propylene/1-butene random copolymer composition were measured in accordance with ASTM D 1894.
• the composite film was held at 40°C for one week and allowed to cool, and the coefficient of static friction and coefficient of dynamic friction thereof were measured in the same manner as in item (4) above.
• Blocking resistance (blocking strength):
• the composite films were held at 50°C for one week and allowed to cool, and the blocking strength was measured in the same manner as in item (6) above.
• a 15 mm wide test piece was cut from the composite film.
• the layers were peeled from each other at one edge of the test piece, and the interlayer bonding strength (peeling strength) between the substrate film layer and the propylene/1-butene random copolymer composition layer was measured by the use of Instron tensile tester in accordance with the T-peel method in which the peeling was conducted at a speed of 300 mm/min.
• a 15 mm wide test piece was cut from each of the composite films heat sealed at the above varied temperatures, and the peeling strength of each test piece was measured by peeling the heat sealed portion at a cross head speed of 200 mm/min.
• Two composite films were piled one upon the other so that their propylene/1-butene random copolymer composition layers contacted each other and heat sealed at each of 80°C, 90°C, 100°C, 110°C, 120°C and 130°C under a pressure of 2 kg/cm 2 for one second. After the heat sealing, a load of 45 g was applied and a peeled distance of the sealed portion was measured.
• Polymerization was carried out for 30 min while continuously supplying propylene and while maintaining the total pressure at 7 kg/cm 2 -G. After the polymerization, deaeration was conducted and a polymer was recovered in a large volume of methanol. The polymer was dried in vacuum at 110°C for 12 hr.
• the yield of the thus obtained polymer (propylene/1-butene random copolymer (PBR-1)) was 39.7 g, so that the polymerization activity was 79 kg-polymer/mmolZr-hr.
• This polymer was analyzed and it was found that the content of structural units derived from 1-butene was 24 mol%, the melt flow rate (measured at 230°C under a load of 2.16 kg in accordance with ASTM D 1238) was 20 g/10 min, the molecular weight distribution (Mw/Mn) determined by GPC was 2.1, the B-value was 1.00, the melting point (Tm) was 91°C and the crystallinity determined by X-ray diffractometry was 40%.
• the yield of the thus obtained polymer (propylene/1-butene random copolymer (PBR-2)) was 33.7 g, so that the polymerization activity was 14 kg-polymer/mmolZr-hr.
• This polymer was analyzed and it was found that the content of structural units derived from 1-butene was 24 mol%, the melt flow rate (measured at 230°C under a load of 2.16 kg in accordance with ASTM D 1238) was 20 g/10 min, the molecular weight distribution (Mw/Mn) determined by GPC was 4.2, the B-value was 0.92, the melting point (Tm) was 110°C and the crystallinity determined by X-ray diffractometry was 48%.
• the molding speed was gradually increased and not only was the maximum laminating speed (m/min) as an index for the laminate moldability determined but also the neck-in (mm) thereat was measured.
• maximum laminating speed used herein means the molding speed at which surging occurs when only the take-off speed is increased while extruding the composition into a layer having a thickness of 20 ⁇ m on a biaxially oriented polypropylene film at a speed of 80 m/min.
• Propylene/1-butene random copolymer composition was prepared in the same manner as in Example 1, except that the amounts of the propylene/1-butene random copolymer (PBR-1) and low-density polyethylene were changed to 80 parts by weight and 20 parts by weight, respectively.
• a composite film was prepared by the same laminate molding as in Example 1 and was subjected to the above tests. The test results are given in Table 1.
• the molding speed was gradually increased and not only was the maximum laminating speed (m/min) as an index for the laminate moldability determined but also the neck-in (mm) thereat was measured.
• a laminate molding of composite film was performed in the same manner as in Example 1, except that the propylene/1-butene random copolymer (PBR-1) was used alone in place of the propylene/1-butene random copolymer composition of Example 1.
• PBR-1 propylene/1-butene random copolymer
• the obtained composite film was subjected to the above tests and the test results are given in Table 1.
• the molding speed was gradually increased and not only was the maximum laminating speed (m/min) as an index for the laminate moldability determined but also the neck-in (mm) thereat was measured.
• Propylene/1-butene random copolymer composition was prepared in the same manner as in Example 1, except that 90 parts by weight of the propylene/1-butene random copolymer (PBR-2) obtained in Production Example 2 was used in place of 90 parts by weight of the propylene/1-butene random copolymer (PBR-1).
• a composite film was prepared by the same laminate molding as in Example 1 and was subjected to the above tests. The test results are given in Table 1.
• the molding speed was gradually increased and not only was the maximum laminating speed (m/min) as an index for the laminate moldability determined but also the neck-in (mm) thereat was measured.
• Propylene/1-butene random copolymer composition was prepared in the same manner as in Example 1, except that 80 parts by weight of the propylene/1-butene random copolymer (PBR-2) obtained in Production Example 2 was used in place of 90 parts by weight of the propylene/1-butene random copolymer (PBR-1) and that the amount of the low-density polyethylene was changed to 20 parts by weight.
• a composite film was prepared by the same laminate molding as in Example 1 and was subjected to the above tests. The test results are given in Table 1.
• the molding speed was gradually increased and not only was the maximum laminating speed (m/min) as an index for the laminate moldability determined but also the neck-in (mm) thereat was measured.

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